JP2017108155A - High pressure chemical vapor deposition apparatuses and methods, and compositions produced therewith - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a composition, reactor apparatus, method and control system for growing epitaxial layers of a group III-nitride alloys, in which a super-atmospheric pressure is used as a process parameter to control the epitaxial layer growth in the case that the identity of alloy layers differ within a heterostructure stack of two or more layers.SOLUTION: A thermodynamically stable semiconductor heterostructure comprises: a first epitaxial layer including a first group III-nitride alloy; and a second epitaxial layer including a second group III-nitride alloy on and contacting the first layer. The first group III-nitride alloy decomposes under an ambient atmospheric pressure at a minimal temperature when the second group III-nitride alloy deposits at an ambient atmospheric pressure. The first group III-nitride alloy does not decompose under a super-atmospheric pressure and at a temperature at which the second group III-nitride alloy deposits.SELECTED DRAWING: Figure 2A

Description

Government Assisted Research or Development This invention was made with US Government support under AFOSR Award # FA9550-07-1-0345. The US government may have certain rights in the invention.

  The present disclosure relates to methods and systems for performing superatmospheric pressure chemical vapor deposition and compositions obtained thereby.

  The possibility of developing a wide spectral range (infrared (IR) to ultraviolet (UV)) photoelectron emitter and detector device structure, and high frequency transistors operating at high power and high temperature, such as group III nitride compounds (eg, nitriding) Has caused great interest in indium, gallium nitride, and aluminum nitride). These materials are produced as epitaxially deposited films, primarily by metal organic chemical vapor deposition (MOVPE) (sometimes also called metal organic chemical vapor deposition (MOCVD or OMCVD)) and molecular beam epitaxy (MBE). . When halogen compounds are utilized, the process is sometimes referred to as halide vapor transport epitaxy (HVTE) or halide vapor phase epitaxy (HVPE). In MOCVD, a reactive gas stream is transported through a reaction region (also called a deposition region), undergoes a gas phase decomposition reaction, the reaction product diffuses toward the substrate surface, and the surface reaction occurs in the deposition region on the substrate. Arise. The reactive precursor fragments are physisorbed and / or chemisorbed on the growth surface, diffuse and nucleate at the reaction site, resulting in film growth.

  However, many other compounds, including indium-rich III-nitrides and oxygen-containing alloys, are very susceptible to thermal decomposition at their optimal kinematic growth temperatures. Indium nitride (InN) has a much higher equilibrium vapor pressure of nitrogen above InN than nitrogen above aluminum nitride (AlN) and nitrogen above gallium nitride (GaN). It is one of the most difficult group III-nitride semiconductor alloys, which makes it difficult to incorporate InN into GaN or AlN based device structures. FIG. 1 shows the pyrolysis pressure for the binary compounds AlN, GaN, and InN as a function of temperature.

Introducing higher concentrations of indium into group III nitride alloys such as In _1-x Ga _x N using low pressure deposition techniques such as MBE or MOCVD due to limitations on thermodynamic stabilization Is a big challenge. Non-equilibrium techniques such as plasma assisted MBE have been applied to temporarily stabilize indium-rich group III-nitride alloys, but these techniques are fundamental to the formation of thermodynamically stable products. Does not solve the general problem. For example, to incorporate an indium-rich In _1-x Ga _x N layer into a wide bandgap III-nitride heterostructure, the indium-rich In _1-x Ga _x N layer has a temperature between 800 ° C. and 1100 ° C. It must be stabilized at typical MOCVD conditions using. However, in a normal low-pressure process, the InN growth temperature needs to be 650 ° C. or lower in order to stabilize the alloy. As the indium content in In _1-x Ga _x N increases, the growth temperature must be increased and the III-V precursor ratio must be adjusted. Thus, the need for growth temperature adjustment for various indium fractions limits the quality of integration of In _1-x GaN layers and / or their inside the same device structure. Currently, only materials containing small amounts of indium (x ≧ 0.75) are made with fairly good quality, but it is believed that there is a solubility gap at higher indium mole fractions. See FK Yam and Z. Hassan, InGaN: An overview of the growth kinetics, physical properties and emission mechanisms, Superlattices and Microstructures 43 (1), pp.1-23 (2008). Accordingly, new systems and methods are needed to provide thermodynamically stable alloys that incorporate heterolayers with varying partial pressures and thermal stability so that useful semiconductor materials can be obtained. .

  In one aspect, a first epitaxial layer comprising a first group III nitride alloy and a second epitaxial layer comprising a second group III nitride alloy on and in contact with the first layer A thermodynamically stable semiconductor heterostructure is provided. The first group III nitride alloy is an alloy that decomposes at atmospheric pressure at the lowest temperature at which the second group III nitride alloy deposits at atmospheric pressure. The first group III nitride alloy is an alloy that does not decompose at superatmospheric pressure and the temperature at which the second group III nitride alloy is deposited.

  In another aspect, a reactor apparatus is provided. The reactor apparatus includes an enclosure that can contain a pressure of up to about 100 bar. The reactor apparatus further includes a substrate carrier adapted to hold the substrate in a reaction region within a flow channel growth reactor, a growth surface on the substrate for growing an epitaxial layer, and A flow channel adapted to direct a flow of the first set of reactive fluids along a first flow direction above the growth surface and an injector adjacent to the reaction region, the injector Is adapted to inject a second set of reactive fluids into the reaction zone, whereby the second set of reactive fluids reacts or decomposes with the first set of reactive fluids. A film of reaction product is deposited on the growth surface.

  In another aspect, providing a growth surface in the reaction region and supplying a first set of reactive fluids across the growth surface into the reaction region in a first flow direction substantially parallel to the growth surface. Supplying a second set of reactive fluids into the reaction region in a second flow direction onto the growth surface, wherein the second flow direction is relative to the first flow direction. Shifting the angle and reacting or decomposing a first set of reactive fluids and a second set of reactive fluids in the reaction region to form an epitaxial layer on the growth surface; Is provided.

  In another aspect, a control system is provided and adapted to supply a plurality of reactive fluids to a superatmospheric reactor and a carrier gas source adapted to supply a carrier gas to the superatmospheric reactor. A plurality of reactive fluid sources, wherein the first reactive fluid source is adapted to supply a first set of reactive fluids to the superatmospheric reactor, and the second to the superatmospheric reactor. A plurality of reactive fluid sources including a second reactive fluid source adapted to supply a set of reactive fluids and initiating a flow of the first set of reactive fluids to the superatmospheric reactor; A plurality of actuators including: a first actuator for stopping, modulating, or a second actuator for starting, stopping, or modulating a flow of a second set of reactive fluids to the superatmospheric reactor And the growth inside the superatmospheric pressure reactor A first set of reactive fluids and a second set of reactive fluids while maintaining a reaction zone comprising a surface, and a substantially constant pressure within the reaction zone and a total volume flow through the reaction zone, And a control device configured to control a plurality of actuators for inserting the gas into the carrier gas.

It is a graph which shows the thermal decomposition pressure regarding a general group III nitride compound semiconductor. FIG. 3 illustrates an exemplary heterostructure grown on a substrate material according to one or more embodiments of the present invention. FIG. 3 illustrates an exemplary heterostructure grown on a substrate material according to one or more embodiments of the present invention. 1 is a cross-sectional view of an exemplary superatmospheric reactor according to one or more embodiments of the present invention. 1 is a cross-sectional view of an exemplary superatmospheric reactor according to one or more embodiments of the present invention. 2 is a graph illustrating a pulse injection scheme according to one or more embodiments of the present invention. 1 is a cross-sectional view illustrating an exemplary superatmospheric pressure reactor incorporated within an external pressure containment vessel, according to one or more embodiments of the present invention. 2 is a graph showing real-time gas composition in a reaction zone monitored by UV-Vis absorption spectroscopy as compared to a reactive fluid injection cycle according to one or more embodiments of the present invention. 2 is a graph illustrating an implantation scheme in which a trimethylindium (TMI) precursor and a trimethylgallium (TMG) precursor are implanted at different times according to one or more embodiments of the present invention. In _1-x Ga _x N of various compositions (x = 0.00, 0.04, 0.09, 0.18, 0.31, and 0.63) according to one or more embodiments of the present invention. It is an X-ray diffraction graph which shows a film. FIG. 6 is a schematic diagram illustrating a method and control system for inserting a pulse of reactive fluid into a carrier gas, and composition control at the atomic level, according to one or more embodiments of the present invention. FIG. 6 is a schematic diagram illustrating a method and control system for inserting a pulse of reactive fluid into a carrier gas, and composition control at the atomic level, according to one or more embodiments of the present invention. FIG. 6 is a schematic diagram illustrating a method and control system for inserting a pulse of reactive fluid into a carrier gas, and composition control at the atomic level, according to one or more embodiments of the present invention. FIG. 6 is a schematic diagram illustrating a method and control system for inserting a pulse of reactive fluid into a carrier gas, and composition control at the atomic level, according to one or more embodiments of the present invention. FIG. 6 is a schematic diagram illustrating a method and control system for inserting a pulse of reactive fluid into a carrier gas, and composition control at the atomic level, according to one or more embodiments of the present invention. 6 is a graph illustrating the relationship between the growth temperature and pressure of InN and In _1-x Ga _x N according to one or more embodiments of the present invention.

  It has been discovered that growth techniques using high pressure provide a means to overcome the existing limitations in epitaxial growth of high quality III-nitride alloy layers. Furthermore, it has been discovered that the growth of indium-rich III-nitride epitaxial layers in the high pressure region (ie, higher than atmospheric pressure, or “superatmospheric pressure”) provides several advantages. The group III nitride alloy epitaxial layer can be grown at a higher growth temperature without thermal decomposition. For example, InN can be grown under a blanket of molecular nitrogen at 750 ° C. to 850 ° C., about 15 atm (compared to less than 600 ° C. for low pressure MOCVD). Analysis of epitaxial layers formed under such conditions shows improved nucleation kinetics at higher growth temperatures, improved surface morphology, and improved microstructure.

Also, under such conditions, In _1-x Ga _x N, In _1-x Al _x N, and / or In _1- are deposited on the AlN, GaN, and / or InN binary layer. _xy Al _x Ga _y N may be grown to produce useful high quality heterostructure semiconductors. On the heterostructure semiconductor thus formed, further, In _1-x Ga _x N, In _1-x Al _x N, In _1-xy Al _x Ga _y N, AlN, GaN, and / or InN Additional layers of may be grown. In particular, operation at higher temperatures and higher pressures allows the growth temperature of In _1-x Ga _x N, In _1-x Al _x N, and / or In _1-xy Al _x Ga _y N to be optimized AlN, To better match GaN and / or InN processing temperatures.

Heterostructure The formation of In _1-x Ga _x N ternary alloy over the entire composition range is achieved when the alloy is in the near infrared (eg InN at about 0.7 eV) to near UV wavelength region (eg 3.5 eV It is very interesting because it allows direct bandgap tuning to GaN). However, from experimental and theoretical predictions, In _1-x Ga _x N ternary alloys have a tendency towards clustering and phase separation and can be thermodynamically and / or kinematically unstable. It is shown. Specifically, a large difference in tetrahedral radii between InN and GaN can induce strain, and this strain can cause the formation of a specific sublattice (phase separation), and the atoms within the sublattice. It has been shown that it can lead to ordering and thereby a departure from homogeneity (nanoclustering). Ayan Kar, Dimitri Alexson, Mitra Dutta. And Michael.A. Stroscio, Evidence of compositional inhomogeneity in In _x Ga _1-x N alloys using ultraviolet and visible Raman spectroscopy, J. Appl.Phys. 104, 073502 (2008), and See IH Ho, GB Stringfellow, Incomplete solubility in nitride alloys, Materials Research Society Symposium Proceedings 449, p. 871 (1997).

  In one embodiment, a thermodynamically stable semiconductor heterostructure composition is provided. As used herein, the term “heterostructure” refers to a layer of semiconductor material comprised of two or more epitaxial layers of semiconductor material that contain different compositions. As used herein, the term “thermodynamically stable heterostructure” refers to a semiconductor that is prepared at high temperature and superatmospheric pressure and then thermodynamically and kinematically stable at atmospheric and atmospheric temperatures. Represents a heterostructure composition. An epitaxial layer of a III-nitride alloy is considered a “semiconductor heterostructure composition” when such a material has an effective structural quality to be suitable for use in a semiconductor material. As used herein, “structural quality” refers to the crystal perfection of an epitaxial layer as measured by the full width at half maximum (“FWHM”) peak width in an X-ray diffraction graph for a Group III nitride composition. For light emitting diodes ("LEDs"), good structural quality is represented by a FWHM of less than about 200 seconds (arcsecond). For laser diodes (“LD”), good structural quality is represented by a FWHM of less than about 50 seconds.

  As used herein, the terms “epitaxial layer” and “epitaxial coating” are synonymous and refer to a single crystal (“monocrystalline”) epitaxial layer of deposited material grown on a suitable substrate. . The epitaxial layer may be grown from a gas or liquid precursor. Since the substrate acts as a seed crystal, the deposited epitaxial film takes the same lattice structure and orientation as the substrate. This film growth process differs from other thin film deposition methods that deposit polycrystalline or amorphous films even on single crystal substrates.

The thermodynamically stable semiconductor heterostructure composition includes a first epitaxial layer made of a first Group III nitride alloy. As used herein, the term “Group III nitride alloy” refers to In _1-x Ga _x N, In _1-x Al _x N, In _1-xy Al _x Ga _y N, AlN, GaN, or InN. Represents any one of The composition further includes a second epitaxial layer comprising a second group III-nitride alloy overlying and in contact with the first layer. As used herein, the term “over and in contact” means that the first layer is covered or incorporated in the second layer and both layers are in contact with each other. . The first group III nitride alloy is an alloy that decomposes at atmospheric pressure at the lowest temperature at which the second group III nitride alloy deposits at atmospheric pressure. Furthermore, the first Group III nitride alloy is stable (ie, does not decompose) kinetically and thermodynamically at superatmospheric pressure and the temperature at which the second Group III nitride alloy is deposited.

  In one embodiment, the composition comprises a first group III-nitride alloy that is AlN, GaN, or InN. In another embodiment, the composition comprises a second group III-nitride alloy that is AlN, GaN, or InN. In yet another embodiment, the composition includes a first epitaxial layer that is AlN, GaN, or InN and a second epitaxial layer that is AlN, GaN, or InN.

One embodiment of the composition according to the invention is In _1-x Ga _x N, In _1-x Al _x N, or In _1-xy Al _x Ga _y N, which is further defined by variables x and y. 1 Group III nitride alloy. In one embodiment, the variables x and y are less than about 0.65, less than about 0.50, less than about 0.35, less than about 0.25, less than about 0.15, or less than about 0.10.

Another embodiment of the composition according to the invention is In _1-x Ga _x N, In _1-x Al _x N, or In _1-xy Al _x Ga _y N, further defined by the variables x and y Includes a second group III-nitride alloy. In one embodiment, the variables x and y are less than about 0.65, less than about 0.50, less than about 0.35, less than about 0.25, less than about 0.15, or less than about 0.10.

In one embodiment, the composition includes a _{In 1-x Ga x N,} In 1-x Al x N , or _{In 1-xy Al x Ga y} N first group III nitride alloy is,, an In _1- and a second group III-nitride alloy that is _x Ga _x N, In _1-x Al _x N, or In _1-xy Al _x Ga _y N. In another embodiment, the composition comprises a first Group III nitride alloy that is AlN, GaN, or InN, and In _1-x Ga _x N, In _1-x Al _x N, or In _1-xy Al. and a second group III nitride alloy that is _x Ga _y N. In yet another embodiment, the composition comprises a _first group III nitride alloy that is In _1-x Ga _x N, In _1-x Al _x M, or In _1-xy Al _x Ga _y N, and AlN , GaN, or InN.

FIG. 2A shows an exemplary embodiment of a heterostructure composition. A first epitaxial layer 13 may be deposited on the substrate material 12. The substrate material 12 may be any suitable nucleation template material, including but not limited to sapphire, silicon carbide, zinc oxide, or silicon. In some embodiments, the first epitaxial layer 13 may be a group III nitride alloy selected from the group consisting of AlN, GaN, and InN. FIG. 2A further shows a second epitaxial layer 15 deposited in contact with the first epitaxial layer 13, where the second epitaxial layer 15 is In _1-x Ga _x N, In _1. It is a group III nitride alloy selected from the group consisting of _-x Al _x N and In _{1 -xy} Al _x Ga _y N. As shown in FIG. 2A, an additional epitaxial layer 17 may further be deposited in contact with the second epitaxial layer 15. The additional epitaxial layer 17 may be a group III nitride alloy (shown) selected from the group consisting of AlN, GaN, and InN, or In _1-x Ga _x N, In _1-x Al _x N. And a group III nitride alloy (not shown) selected from the group consisting of In _1-xy Al _x Ga _y N.

Another exemplary embodiment of a heterostructure composition is shown in FIG. 2B. A first epitaxial layer 19 may be deposited on the substrate material 12. The substrate material 12 may be any suitable nucleation template material, including but not limited to sapphire, silicon carbide, zinc oxide, or silicon. In some embodiments, the first epitaxial layer 19 may be a group III nitride alloy selected from the group consisting of AlN, GaN, and InN. FIG. 2B further shows a second epitaxial layer 21 deposited in contact with the first epitaxial layer 19, where the second epitaxial layer 19 is In _1-x Ga _x N, In _1. It is a group III nitride alloy selected from the group consisting of _-x Al _x N and In _{1 -xy} Al _x Ga _y N. As seen in FIG. 2B, an additional epitaxial layer 23 may also be deposited in contact on the second epitaxial layer 21. The additional epitaxial layer 23 may be a group III nitride alloy (shown) selected from the group consisting of AlN, GaN, and InN, or In _1-x Ga _x N, In _1-x Al _x N. And a group III nitride alloy selected from the group consisting of In _1-xy Al _x Ga _y N (not shown).

Reactor Design In one aspect, a reactor apparatus is provided for growing a III-nitride alloy epitaxial layer having an effective structural quality suitable for use with semiconductor materials. The design of a reactor for epitaxial film growth at superatmospheric pressure takes into account hydrodynamics, chemical reactions, reaction rates, and mass transport principles. More specifically, this design takes into account reactant gas and surface reaction chemistry under epitaxial film growth conditions.

  A reactor apparatus for growing an epitaxial layer on a substrate having a growth surface includes a substrate carrier adapted to hold the substrate in a reaction region within the reactor, and when the substrate is attached to the substrate carrier And a flow channel adapted to direct a flow of the first set of reactive fluids along a first flow direction above the growth surface of the substrate. An injector may be provided adjacent to the reaction zone and adapted to inject a second set of reactive fluids into the reaction zone so that the second set of reactive fluids is in the first set. The reactive fluid is reacted or decomposed to deposit a film of reaction product on the growth surface. The reactor apparatus may further comprise an enclosure capable of confining a pressure of up to about 100 bar.

  The term “set”, as used herein with reference to a reactive fluid, generally represents a reactive fluid having one or more components. Thus, a “set of fluids” may include a volume of reactive fluid consisting only of a carrier gas or a single reactive fluid. It may also include a fluid comprising a plurality of components or reactive fluids.

  In some embodiments, the substrate carrier is adapted to hold the substrate in a first plane parallel to the first flow direction. As used herein, the terms “parallel” and “substantially parallel” are intended to convey reactive fluid from the upstream end of the substrate toward the downstream end of the substrate over a substantially flat substrate plane. Represents a fluid flow direction with a flow vector.

  In some embodiments, the flow vector may have an angle of incidence relative to the plane of the substrate, but the angle of incidence relative to the growth surface is greater than about 45 degrees, greater than about 60 degrees, about 75 degrees. It may be greater than or greater than about 90 degrees. An incident angle of about 90 degrees is considered parallel.

  In some embodiments, the injector for injecting the second set of reactive fluids into the reaction region is such that the second set of reactive fluids is uniformly distributed across the growth surface of the substrate. Have been adapted. In some embodiments, the injector may include a porous ceramic material. Alternatively, the injector may comprise a dispersion block having a plurality of conduits therethrough. In another embodiment, the injector is adapted to direct the reactive fluid to the reaction region or growth surface.

  Further, in some embodiments, the injector may be configured to inject the second reactive fluid into the reactor in a direction substantially perpendicular to the first flow direction. As used herein, the terms “vertical” and “substantially vertical” refer to a fluid flow direction in which the flow vector forms a large angle of incidence with respect to the flow direction of the substrate or first reactive fluid.

  In some embodiments, the flow vector directs the reactive fluid into a substantially flat substrate surface (ie, the plane on which the coating is deposited). The angle of incidence relative to the plane of the substrate may be less than about 45 degrees, less than about 30 degrees, less than about 15 degrees, or less than about 0 degrees. An incident angle of about 0 degrees is considered vertical.

  In some embodiments, the flow channel may be fluidly connected to the Group V precursor source and the injector may be fluidly connected to the Group III precursor source. Alternatively, the flow channel may be fluidly connected to the group III precursor source and the injector may be fluidly connected to the group V precursor source. As used herein, the term “precursor source” means a source of reactive fluid. For example, the precursor source may include, but is not limited to, organometallic precursors such as trimethylindium and trimethylgallium, liquid precursors such as hydrazine, and / or gaseous precursors such as ammonia and silane.

  In some embodiments, the first set of reactive fluids and the second set of reactive fluids are transported to the reaction region in a temporally and spatially controlled manner as a pulsed or modulated flow. And a control device for controlling the flow of the first set of reactive fluids and the second set of reactive fluids. As used herein, the term “pulse” generally refers to a volume of reactive fluid having a temporally and / or spatially controlled flux, and thus a pulse is a pulse inserted into it. Having a starting and ending point that is separate from the continuous carrier gas stream. Thus, in one embodiment, the controller may be adapted to pulse the reactive fluid into a continuous supply stream of carrier gas for transport to the reaction zone, which pulse is It concentrates the distribution of reactive fluid in it in time and space.

  One embodiment of a superatmospheric reactor is shown in FIGS. 3A and 3B. The growth reactor 10 may be incorporated in an external pressure vessel (not shown). The growth reactor 10 includes a flow channel 26 that transports a reactive fluid in the direction of the substrate 12. The substrate 12 may be any substrate suitable for the growth of group III nitride alloy epitaxial layers, such as sapphire, silicon carbide, silicon, or zinc oxide. In some examples, a first epitaxial layer comprising a Group III nitride alloy is deposited, thereby functioning as a substrate for growth of the second epitaxial layer. In other embodiments, an additional epitaxial layer comprising a III-nitride alloy may serve as a substrate for subsequent epitaxial layer growth. The substrate 12 is attached to a substrate carrier 18 that holds the substrate 12 such that the growth surface of the substrate 12 lies in a plane substantially parallel to the flow direction of the flow channel 26. The substrate may have a small tilt angle with respect to the flow channel in order to provide an effective gas flow reaction rate and surface replenisher supply to optimize the chemical reaction at the growth surface.

  The shaft 16 may be attached to a substrate carrier 18 and may be mechanically coupled to a motor so that the substrate carrier 18 and the substrate 12 rotate at an angle in the plane of the growth surface. In some embodiments of the invention, shaft 16 rotates substrate 12 and substrate carrier 18 at a low rotational speed, preferably between 1 and 20 Hz. In other embodiments, higher rotational speeds are used if and when a need arises to improve growth rates, surface chemistry, and / or film uniformity. Also good. Thus, in one embodiment, the growth reactor 10 may further comprise a device adapted to rotate the substrate carrier.

  A reaction region 32 for growing the epitaxial layer is provided above the substrate 12. A showerhead injector 24 may be disposed above the reaction region 32 on the opposite side of the substrate 12. The showerhead injector 24 may be adapted to inject a second set of reactive fluids onto the surface of the substrate in a direction perpendicular to the flow channel 26. The showerhead injector 24 may generally be adapted to uniformly distribute the second set of reactive fluids across the growth surface. In some embodiments, the showerhead injector 24 may include a porous glass, ceramic, or metallic material. In other embodiments, the showerhead injector 24 may comprise a distribution block having a plurality of conduits extending from the chamber 22 to the reaction region 32. A conduit 20 may be provided to supply a second set of reactive fluids to the chamber 22.

In some embodiments, the reactive fluid transported through the flow channel 26 includes, but is not limited to, ammonia [NH ₃ ], dimethyl hydrazine [(CH ₃ ) ₂ N (NH ₂ )], or t-butylamine [ A V group precursor containing (CH ₃ ) ₃ CNH ₂ ] may be used. The second set of reactive fluids includes, but is not limited to, trimethylindium [In (CH ₃ ) ₃ ] (“TMI”), trimethylaluminum [Al (CH ₃ ) ₃ ] (“TMA”), or trimethylgallium. Group III reactive precursors including organometallic precursors such as [Ga (CH ₃ ) ₃ ] (“TMG”) may also be included. The reactive fluid may be inserted into the carrier gas stream or injected in liquid form and transported to the reaction zone or substrate.

  The temperature of the reaction zone 32 and the temperature of the substrate 12 may be controlled by applying heat inductively or conductively to the substrate carrier 18 via the heating element 14. The pressure in the reaction zone 32 may be controlled by adjusting the pressure of the carrier gas and inert gas between the growth reactor 10 and the external pressure vessel. Differential pressure control can be employed between the growth reactor 10 and the external pressure vessel for stable operation. The growth reactor 10 may be operable at or below atmospheric pressure, but may preferably be operated at superatmospheric pressure including a reactor pressure region of 2 to 100 bar. In yet another embodiment, the growth reactor 10 may be operated in a reaction pressure region of 2-30 bar.

  A second heating element 28 may be provided upstream of the substrate 12 to allow preheating of the first set of reactive fluids. This heating element may provide independent control of the decomposition reaction rate of the first set of reactive fluids. Similarly, a third heating element 30 may be provided to preheat the second set of reactive fluids, which allows control of the decomposition reaction rate of the second set of reactive fluids. . The heating element 30 may be isolated from the reaction region 32 so as not to act on the reactive fluid injected through the flow channel 26 and may allow independent control of the decomposition reaction rate of each set of reactive fluids.

  As shown in FIGS. 3A and 3B, in order to load and / or remove the substrate 12 from the growth reactor 10 without exposing the growth reactor 10 to the ambient atmosphere, “ A “load lock” system may be provided. The system may utilize an isolation chamber 34 for inserting or removing the substrate 12 from the growth reactor 10.

  Another embodiment of a superatmospheric pressure reactor 80 is shown in FIG. In this embodiment, the substrate carrier 86 may be inductively heated by RF coupling by an RF coil 84 surrounding the substrate carrier 86. The second heater 82 may be disposed adjacent to the flow path of the reactive fluid and may heat the reactive fluid before the reactive fluid reaches the reaction region.

Growth Methods In another aspect, a method for growing epitaxial layers and heterostructures on a substrate is provided. First, the growth surface of the substrate, which may be arranged on the substrate carrier, faces the reaction region. Thereafter, a first reactive fluid may be supplied into the reaction region in a first flow direction parallel to the growth surface, over the growth surface, and above the growth surface. Two flow directions may be fed onto the growth surface into the reaction zone, where the second flow direction is offset in angle from the first flow direction. Without being limited by any structural chemistry theory, the first reactive fluid and the second reactive fluid may then be decomposed into precursor fragments within the reaction zone, which are then grown on the growth surface. And can be chemisorbed and / or physisorbed onto the growth surface of the substrate. The term “shift angle” is used herein to characterize the flow direction and represents a flow vector that may intersect at an angle.

  In some embodiments, the method further comprises maintaining a superatmospheric pressure within the reaction zone. In some embodiments, the growth of the III-nitride alloy epitaxial layer may be performed at superatmospheric pressures between 2 and 100 bar in the reaction region. In another embodiment, the growth of the III-nitride alloy epitaxial layer may be performed at superatmospheric pressure between 2 and 30 bar in the reaction region. In general, the growth reactor pressure can be maintained by supplying a carrier gas into the reaction zone at the desired pressure and flow rate.

  As will be discussed in more detail later, in some embodiments, the pressure in the reaction region, and the total volume flow rate of the carrier gas and reactive fluid are constant during the epitaxial film growth of a particular group III-nitride alloy. It can be controlled to be kept. To accomplish this, a reactive fluid may be inserted into the carrier gas so that the overall flow rate in the reaction zone is kept constant. The insertion and injection scheme can be tightly controlled to prevent variations in the total volume flow rate of the carrier gas and reactive fluid through the reaction region. Thus, the pulse of reactive fluid replaces a volume of carrier gas that is substantially equal to the volume occupied by the pulse at the operating pressure. Each particular epitaxial layer of group III nitride alloy to be grown may require a different pressure region. Transitions between different Group III-nitride alloys grown in different pressure regions may be achieved by utilizing a controlled pressure transition region, which affects the quality of the growing epitaxial layer The pressure increases / decreases without causing possible pressure fluctuations.

  In some embodiments, the method further includes rotating the growth surface within the reaction zone while supplying the first reactive fluid and the second reactive fluid to the reaction zone. Rotation can help achieve uniform distribution of the reactive fluid across the growth surface.

  Further, in some embodiments, the method includes the first reactive fluid at the first time point such that the first reactive fluid and the second reactive fluid are present in the reaction zone at substantially the same time. Injecting a reactive fluid into the reactor and injecting a second reactive fluid into the reactor at a second time point. The term “substantially simultaneous” as used herein to denote the relative arrival time of a reactive fluid, even if one of the reactive fluids arrives first in the reaction region, or It generally means that the first reactive fluid and the second reactive fluid are present in the reaction region at the same time, even if they exist in the reaction region for a longer period of time than the other reactive fluid. In some embodiments, the method further includes monitoring and controlling the composition of the gas phase components and / or reactive fluid in the reaction zone in real time.

  In some embodiments, the first set of reactive fluids and the second set of reactive fluids comprise alternating Group III and Group V reactive fluids.

  Referring again to FIG. 3A, the method includes transporting a first set of reactive fluids to the reaction region 32 in a flow direction parallel to the growth surface and over the growth surface across the growth surface of the substrate 12. May be included. For example, a first set of reactive fluids may be transported to the reaction region 32 through the flow channel 26 as shown in FIGS. 3A and 3B. A second set of reactive fluids may be injected onto the growth surface of the substrate 12 into the reaction region 32 in the second flow direction. For example, a second set of reactive fluids may be injected into the reaction region 32 through the tightly coupled showerhead injector 24 as shown in FIG. 3A. The second flow direction may be substantially perpendicular to the flow direction of the first set of reactive fluids.

  In some embodiments, the reactive fluid may be injected into the reaction region 32 as a timing pulse (ie, the component gas flux is controlled in time). The growth reactor 10 of FIGS. 3A and 3B may be particularly well suited for such an implantation method.

FIG. 4 shows a pulse injection scheme in which reactive fluid is injected into a common flow path. The reader may assume by way of example that each reactive fluid is injected as alternating pulses through the flow channel 26 of the growth reactor 10 of FIG. As shown in FIG. 4, a pulse of TMI may be injected into a carrier gas stream (eg, N ₂ ), followed by an ammonia pulse. In this example, the total gas flow rate (the sum of the carrier gas and the inserted reactive fluid) and the pressure in the reaction zone may always be kept constant.

  After a predetermined period, each reaction component reaches the reaction region and the growth surface of the substrate 12. While the pulse is transported from the injector to the substrate 12, the pulse may spread due to a decrease in flow velocity at the boundary of the flow channel 26. This may cause some of the inserted reactive fluid pulses to overlap, such as in this example where both ammonia and TMI are present in the flow channel 26, and thus before the reactive fluid reaches the substrate 12. Gas phase reactions involving reactive fluids may occur.

  By injecting the Group III and V reactive fluids into the reaction region 32 through different paths, the growth reactor 10 of FIGS. 3A and 3B can tightly control the conditions under which the epitaxial layer is produced. It should be understood that it may be well suited to For example, separation of the injection path of reactive fluids (eg, Group III and Group V reactive fluids) can greatly reduce or eliminate the possibility of reactive fluid reaction within the flow channel 26. , May allow introduction of each reactive fluid at optimal pulse timing and / or narrower pulse intervals. This may allow optimization of the use of reactive fluid material with each pulse and a faster growth rate.

  In some embodiments, the pressure in the reaction zone, and the total volume flow of reactive fluid and carrier gas through the reactor, may remain constant throughout the growth process of a particular component coating / alloy configuration. The reaction while balancing the carrier gas flow rate to maintain a substantially constant total volume flow through the reactor, a substantially constant average flow rate, and / or a substantially constant pressure in the reaction zone. A control system may be provided to inject metered pulses of reactive fluid into the vessel. Accordingly, the reactive fluid may be injected into the carrier gas stream as metered pulses, and the duration and amplitude of each pulse may be metered. The amplitude of the pulse corresponds to the average volume flow of the reactive fluid during the pulse, and the product of duration and amplitude corresponds to the total volume of reactive fluid for that pulse. In addition, each pulse may be spaced from a subsequent pulse by a predetermined time during which only carrier gas is injected into the reactor. Each of these control parameters (duration, amplitude, and / or interval) can be automatically adjusted and controlled depending on the predetermined process parameters of each layer alloy and its composition. Accordingly, one embodiment of the method performed by the present invention includes monitoring and controlling the compositional and spatial distribution of gaseous components within the reaction zone in real time.

Control System In another aspect, a control system for growing semiconductor quality heterostructures using superatmospheric growth conditions may be provided. The control system may control the injection of the first and second reactive fluids into a growth reactor having a reaction region for growing a film on the substrate. The control system includes a carrier gas source adapted to supply a carrier gas to the superatmospheric reactor and a plurality of reactive fluid sources adapted to supply a plurality of reactive fluids to the superatmospheric reactor. And the reactive fluid source is adapted to supply a first reactive fluid to the superatmospheric reactor and a second reactive fluid to the superatmospheric reactor. And a second reactive fluid source adapted to supply the second reactive fluid source. A plurality of actuators may also be provided, the first actuator for flowing a first set of reactive fluids in the superatmospheric reactor and a second set of reactions to the superatmospheric reactor. And a second actuator for starting and stopping the flow of the sexual fluid. Also, the first set of reactive fluids and the second set of reactive fluids are used as carrier gases while maintaining a substantially constant pressure in the reaction zone and a total volume flow through the reaction zone. A control device may be provided or configured to control a plurality of actuators to be inserted.

  In some embodiments, the control system may be configured to supply a carrier gas at a first constant volumetric flow rate through the reaction zone in a non-reactive phase, wherein the first constant volumetric flow rate is the total constant flow rate. It is substantially equal to the volume flow rate. During the reaction phase, the volume flow of the carrier gas through the reaction zone may be reduced to offset the volume flow of the reactive fluid through the reaction zone. Furthermore, the control system may be configured to maintain a constant pressure in the reaction zone of about 2 bar to about 100 bar, or about 2 bar to about 30 bar. As used herein, the terms “constant pressure” and “substantially constant pressure” may be used interchangeably, and the pressure in the reaction zone is greatly increased when a film is grown on a substrate. Generally represents methods and systems that do not change or vary. Thus, the pressure in the reaction zone is the same during the non-reaction phase (ie when only the carrier gas is fed through the reaction zone) and during the reaction phase (ie when the reactive fluid is inserted into the carrier gas). Or differ by less than about 0.01 bar, the pressure in the reaction zone is “substantially constant”.

  In some embodiments, the control system may be used to inject Group III and Group V reactive fluids into the reactor.

  A control system for injecting a pulse of reactive fluid into a carrier gas stream is shown in FIGS. 9A-9E. The control system includes a plurality of valves to control the flow of carrier gas (eg, nitrogen) and reactive fluid toward the reactor 100 through the fluid circuit. Alternatively, a more sophisticated mechanical injection system, such as a rotating cylinder injector that mimics the function of multiple valves or other types of manifolds, may be used as an equivalent. Carrier gas may be supplied to the circuit from push gas supply 104 and compressed gas supply 108. The push gas supply 104 may supply the carrier gas to the circuit at a sufficient flow rate that matches a predetermined flow rate for the reactor 100. The compressed gas source 108 supplies carrier gas to the circuit as needed to maintain the required pressure in the reaction zone and / or to pressurize a portion of the fluid circuit. Can do. It should be noted that the control system shown in FIGS. 9A-9E is merely intended to illustrate one possible control system for inserting a pulse of reactive gas into a carrier gas. Various other fluid circuit configurations for inserting reactive fluids into the carrier gas stream may be used to perform the methods described herein.

  FIG. 9A illustrates one possible valve control configuration that can control the flow path of carrier gas and reactive fluid when multiple valves are open or closed in the default position. In this configuration, a constant flow of carrier gas can be supplied to the reactor 100 while the reactive fluid can define a flow path towards the outlet.

  To prepare a “pulse” of reactive fluid, the valve may be opened and closed as shown by the flow path in FIG. 9B. Although the carrier gas flow does not change, the reactive fluid flow may redefine the flow path by opening and closing a valve to open a fluid circuit comprising the charge reservoir 102 (feed reservoir 102); The charge reservoir 102 may be configured to include or insert a precisely metered volume of reactive fluid into the carrier gas supplied to the reactor 100. Immediately after the circuit is purged, the valve may be closed to fill the charge reservoir 102 with a predetermined volume and pressure of reactive fluid from the precursor source 106, as shown in FIG. 9C. After a predetermined volume of reactive fluid has been supplied to the charge reservoir 102, the volume of reactive fluid can be compressed with a carrier gas from the compressed gas supply 108, as shown in FIG. Can be closely matched to the pressure in the reactor region 100 and the fluid circuit supplied by.

  To supply a pulse of reactive fluid in the charge reservoir 102 to the reactor 100, as shown in FIG. 9E, by opening and closing appropriate valves to direct flow through the charge reservoir 102 to the reactor 100, The flow path of the carrier gas flow from the push gas supply 104 may be redefined. The carrier gas conveys a pulse of reactive fluid to the reactor 100 toward the reaction region, where the reactive fluid may react with another reactive fluid.

  It should now be understood that the above process may be repeated as necessary to supply a continuous pulse of reactive fluid to the reactor 100. Further, the charge reservoir 102 may be filled to various levels to change the volume concentration of the reactive fluid pulse supplied to the reactor region of the reactor 100. Also, a portion of the carrier gas from the push gas supply 104 may bypass the charge reservoir 102 to change the pulse amplitude or volume flow.

  The control system may include a programmable controller that operates the valves according to a programmable schedule. For example, the controller may provide control of the aforementioned parameters of pulse duration, pulse amplitude, and pulse interval.

  In addition, advanced real-time optical diagnostics (e.g. UV-VIS-IR, FTIR, Raman spectroscopy) may be integrated with the controller, and as input to the controller, real-time characteristic data of the epitaxial film and closed-loop feedback control data. I will provide a. Such characterization processes and control methods are described in V. Woods and N. Dietz. InN growth by high-pressures chemical vapor deposition: Real-time optical growth characterization, Mater. Sci. & Eng. B 127 (2-3) pp 239-250 (2006), IP Herman, Optical Diagnositcs for thin Film Processing (Academic Press Inc., New York, 1996), D. E, Aspnes and N. Dietz, Optical Approaches for Controlling Epitaxial Growth, Applied Surface Science 130 -132 pp. 367-376 (1998) and N. Dietz, Real-time optical Characterization of thin film growth, Mater. Sci. & Eng. B87 (l), pp. 1-22 (2001) ing.

  Having described the invention, the following examples are presented to illustrate the application of the invention to the growth of indium-rich group III-nitride alloys. These specific examples and compositions are not intended to limit the scope for Group III nitrides or heterostructures. The methods, reactors, and control systems described herein may be applied to any material system that has significantly different partial pressures of coating alloy components, such as oxide-based dielectrics or other compound semiconductors.

Example 1: Control of Gas and Surface Reaction Chemistry For the above HPCVD reactor, various absorption spectroscopy methods such as UV-Vis absorption spectroscopy were used to analyze the reaction rate of gas phase components above the growth surface. obtain. Several analytical methods are described in V. Woods and N. Dietz, InN growth by high-pressures chemical vapor deposition: Real-time optical growth characterization, Mater. Sci. & Eng. B 127 (2-3) pp.239- 250 (2006).

  FIG. 6 shows a typical reactive fluid flux injection scheme used during InGaN growth and a real-time UV-Vis absorption waveform monitored above the growth surface at 222.8 nm under steady state InGaN growth conditions. Is illustrated. In this example, a TMI reactive fluid and a TMG reactive fluid were injected simultaneously.

The upper part of the graph shows the precursor flux (precursor flux) of the reactive fluid and the carrier gas with respect to time. As shown in this graph, the total volume flow through the reactor remained constant throughout the injection cycle sequence. Three injection cycles are shown. Each cycle began with a pulse of NH ₃ inserted into the carrier gas. The width of the pulse represents the duration of the pulse (1.5 seconds in this example) and the area within the pulse represents the total volume of NH ₃ inserted into the carrier gas. The NH ₃ pulse was followed by a period in which only the carrier gas was injected into the reactor. Immediately thereafter, a pulse of the second reactive fluid, namely TMI and TMG, was injected into the carrier gas. The period between NH ₃ and TMI / TMG pulses may be referred to as a pulse interval. A second pulse interval was provided between the TMI / TMG injection and the next NH ₃ pulse. The next injection of NH ₃ indicated the start of a new injection cycle.

The lower part of the graph of FIG. 6 shows the UV absorption waveform in real time at a wavelength where the reactive fluid exhibits characteristic absorption (λ _max = 222.8 nm in this example). The arrival of the reactive fluid above the growth surface can be observed with a UV-Vis waveform and can be correlated to each reactive fluid component. Control of the injection sequence at the top of the graph utilizing real-time UV-Vis waveform analysis allows for rigorous design of gas phase and surface reactions, which is an essential element for optimizing process conditions. To optimize growth conditions, adjustment of the pulse interval between reactive fluids and the length of each reactive fluid pulse may be used as process control parameters.

  As shown in FIG. 7, TMI and TMG may be injected as separate pulses to provide additional process control parameters. Individual pulse implantation may be particularly beneficial for the growth of ternary alloys such as InAlGaN. In particular, such growth schemes may be employed for ternary InGaN alloy formation to control phase separation and to compensate for the different growth chemistry of TMI and TMG at the quasi-monolayer level. Good. For example, each sequence may be uniquely tailored to the gas and surface chemistry of the alloy being formed, for example, each sequence may have a unique timing for the pulse interval. Also, by adjusting the precursor pulse length, each sequence can have a unique group V / III reactive fluid ratio adjusted to a specific partial pressure. Each sequence may be repeated multiple times to deposit a specific amount of material to form the target material composition, and each sequence can be adjusted to material alloying / mixing process, phase separation process of different materials Or the formation of 2D and 3D nanocomposites, quantum dots, or quantum wells.

Example 2: InGaN growth by HPCVD The initial results for the structural properties of In _1-x Ga _x N layers grown by HPCVD are shown in FIG. FIG. 8 shows the X-ray diffraction (XRD) results of an In _1-x Ga _x N layer grown at the same growth temperature and with a reactor pressure of 15 bar. The gallium composition was varied at x = 0.0, 0.04, 0.09, 0.18, 0.31, and 0.63. The growth temperature was kept constant for x values less than x = 0.4 and increased by 50 ° C. for x = 0.63. The position and full width at half maximum (FWHM) of the InGaN (0002) Bragg reflection is a measure for the composition and structural quality of the grown layer. As used herein, “structural quality” refers to the crystal perfection of an epitaxial layer as measured by FWHM. For LEDs, good structural quality is represented by a FWHM of less than about 200 seconds. For LD, good structural quality is represented by a FWHM of less than about 50 seconds. The binary InN alloy (x = 0.0) has an InN (0002) Bragg reflection with a FWHM of less than 200 seconds and is similar to a value suitable for use in LEDs reported for MBE growth layers. Value. As shown in FIG. 7, with increasing gallium incorporation, an InGaN (0002) Bragg reflection (decrease in lattice constant) transitioning to a higher 2Θ value and an increase in Bragg reflection FWHM were observed.

  Two Bragg reflections were observed indicating the presence of different phases of different compositions for gallium concentrations in the range of x = 0.1 to x = 0.30. However, InGaN layers within the same composition range grown on sapphire substrates showed single-phase behavior when demonstrated by InGaN (0002) Bragg reflection.

Example 3 Relationship between Reactor Pressure and Growth Temperature Initial results regarding the relationship between growth temperature and reactor pressure for InN and In _0.85 Ga _0.15 N are shown in FIG. As shown in FIG. 10, the possible growth temperature for InN can be increased at about 6.6 ° C./bar, resulting in an InN growth temperature of about 880 ° C. at a reactor pressure of 20 bar. For In _1-x Ga _x N at x = 0.15, the slope (represented by an increase in growth temperature as a linear function of pressure increase) decreases slightly to about 6.0 ° C./bar. . The growth temperature increasing with reactor pressure shown in FIG. 10 is for growth of In _1-x Ga _x N device structures that must integrate In _1-x Ga _x N epitaxial layers with a wide composition range (x). It shows the benefits of HPCVD.

  Although the present invention has been described above, it is clear that the same method can be modified in many ways. Such variations are not to be regarded as a departure from the spirit and scope of the invention, and all modifications apparent to those skilled in the art are intended to be included within the scope of the appended claims.

Claims (40)

A first epitaxial layer comprising a first group III nitride alloy;
A second epitaxial layer comprising a second III-nitride alloy overlying and in contact with the first layer;
The first group III nitride alloy is an alloy that decomposes at atmospheric pressure at the lowest temperature at which the second group III nitride alloy deposits at atmospheric pressure;
The first group III nitride alloy is a thermodynamically stable semiconductor heterostructure that is an alloy that does not decompose at superatmospheric pressure and the temperature at which the second group III nitride alloy is deposited.   The thermodynamically stable semiconductor heterostructure of claim 1, wherein the first group III nitride alloy is aluminum nitride, gallium nitride, or indium nitride.   The thermodynamically stable semiconductor heterostructure of claim 1, wherein the second group III nitride alloy is aluminum nitride, gallium nitride, or indium nitride. 2. The heat of claim 1, wherein the first group III nitride alloy is one of In _1-x Ga _x N, In _1-x Al _x N, or In _1-xy Al _x Ga _y N. Dynamically stable semiconductor heterostructure.   The thermodynamically stable semiconductor heterostructure of claim 4, wherein x and y are less than about 0.65.   The thermodynamically stable semiconductor heterostructure of claim 4, wherein x and y are less than about 0.50.   The thermodynamically stable semiconductor heterostructure of claim 4, wherein x and y are less than about 0.35.   The thermodynamically stable semiconductor heterostructure of claim 4, wherein x and y are less than about 0.25.   The thermodynamically stable semiconductor heterostructure of claim 4, wherein x and y are less than about 0.15.   The thermodynamically stable semiconductor heterostructure of claim 4, wherein x and y are less than about 0.10. 2. The heat of claim 1, wherein the second group III nitride alloy is one of In _1-x Ga _x N, In _1-x Al _x N, or In _1-xy Al _x Ga _y N. Dynamically stable semiconductor heterostructure.   The thermodynamically stable semiconductor heterostructure of claim 11, wherein x and y are less than about 0.65.   The thermodynamically stable semiconductor heterostructure of claim 11, wherein x and y are less than about 0.50.   The thermodynamically stable semiconductor heterostructure of claim 11, wherein x and y are less than about 0.35.   The thermodynamically stable semiconductor heterostructure of claim 11, wherein x and y are less than about 0.25.   The thermodynamically stable semiconductor heterostructure of claim 11, wherein x and y are less than about 0.15.   The thermodynamically stable semiconductor heterostructure of claim 11, wherein x and y are less than about 0.10. An enclosure capable of confining a pressure of up to about 100 bar;
A substrate carrier adapted to hold the substrate in the reaction region within the flow channel growth reactor;
A growth surface on the substrate for growing an epitaxial layer;
A flow channel adapted to direct a flow of a first set of reactive fluids along a first flow direction above the growth surface;
An injector adjacent to the reaction zone, the injector being adapted to inject a second set of reactive fluids into the reaction zone, whereby the second set of reactive fluids Reactor apparatus that reacts with or decomposes with the first set of reactive fluids to deposit a film of reaction product on the growth surface.   The reactor apparatus of claim 18, wherein the substrate carrier is adapted to hold the substrate in a first plane substantially parallel to the first flow direction.   The reactor apparatus of claim 18, wherein the injector is adapted to uniformly distribute the second reactive fluid across the growth surface.   The reactor apparatus of claim 18, wherein the injector comprises a porous material.   The reactor apparatus of claim 18, wherein the injector comprises a dispersion block having a plurality of conduits therethrough.   The reactor apparatus of claim 18, wherein the injector is adapted to direct a reactive fluid toward the reaction region or the growth surface.   The reactor apparatus of claim 18, wherein the injector is adapted to direct a reactive fluid toward the reactor in a direction substantially perpendicular to the first flow direction.   The reactor apparatus of claim 18, wherein one of the injector or the flow channel is fluidly connected to a Group V reactive fluid source.   26. The reactor apparatus of claim 25, wherein the other of the injector or the flow channel is fluidly connected to a group III reactive fluid source.   Further comprising a controller adapted to pulse reactive fluid into the continuous feed stream of carrier gas for transport to the reaction zone, wherein the pulse is the reaction in the continuous feed stream. The reactor apparatus according to claim 18, wherein the distribution of the sex fluid is concentrated temporally and spatially.   The reactor apparatus of claim 18, further comprising a device adapted to rotate the substrate carrier.   The reaction of claim 18, wherein the injector is configured to inject the second set of reactive fluids into the reactor in a direction substantially perpendicular to the first flow direction. Equipment. Providing a growth surface in the reaction region;
Supplying a first set of reactive fluids across the growth surface into the reaction region in a first flow direction substantially parallel to the growth surface;
Supplying a second set of reactive fluids onto the growth surface in a second flow direction into the reaction region, wherein the second flow direction is relative to the first flow direction. Step to shift the angle,
Reacting or decomposing the first set of reactive fluids and the second set of reactive fluids in the reaction region to form an epitaxial layer on the growth surface.   31. The method of claim 30, further comprising maintaining a pressure of about 2 bar to 100 bar in the reaction zone.   32. The method of claim 30, further comprising rotating the growth surface within the reaction region.   The first set of reactive fluids at a first point in time such that the first set of reactive fluids and the second set of reactive fluids are present in the reaction zone substantially simultaneously. 32. The method of claim 30, further comprising injecting into the reactor and injecting the second set of reactive fluids into the reactor at a second time point.   32. The method of claim 30, further comprising maintaining a total volume flow through the reaction zone.   31. The method of claim 30, wherein the first set of reactive fluids and the second set of reactive fluids comprise alternating one set of group III reactive fluids and one set of group V reactive fluids. Method.   36. The method of claim 35, further comprising monitoring and controlling the compositional and spatial distribution of gaseous components within the reaction zone in real time. A carrier gas source adapted to supply a carrier gas to the superatmospheric pressure reactor;
A plurality of reactive fluid sources adapted to supply a plurality of reactive fluids to the superatmospheric reactor, adapted to supply a first set of reactive fluids to the superatmospheric reactor. A plurality of reactive fluids including a first reactive fluid source being adapted and a second reactive fluid source adapted to supply a second set of reactive fluids to the superatmospheric pressure reactor The source,
A first actuator for initiating, stopping, or modulating the flow of the first set of reactive fluids to the superatmospheric reactor, and the second set of reactive fluids to the superatmospheric reactor. A plurality of actuators including a second actuator for starting, stopping or modulating the flow of
A reaction zone comprising a growth surface inside the superatmospheric pressure reactor;
Maintaining the first set of reactive fluids and the second set of reactive fluids while maintaining a substantially constant pressure in the reaction zone and a total volume flow through the reaction zone; A control system configured to control the plurality of actuators for insertion into a carrier gas.   The control system is configured to supply a carrier gas at a first constant volumetric flow rate through the reaction region in a non-reactive phase, wherein the first constant volumetric flow rate is substantially equal to the total volumetric flow rate. 38. The control system of claim 37, wherein   38. The first set of reactive fluids and the second set of reactive fluids alternately comprise a set of group III reactive fluids and a set of group V reactive fluids. Control system.   38. The control system of claim 37, configured to maintain a pressure of about 2 bar to about 100 bar in the reaction zone.

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